丙酸发酵的研究

北京丙酸杆菌(Propionibacrerium beijingense)不能利用无机氮。蛋白胨和酵母膏的种类对该菌生长和产酸的影响显著,其中以酵母膏最好,浓度以l一2％为宜。丙酸发酵最适温度为25一30℃,最适pH为6．5,葡萄糖浓度以1-2％为佳。使用下列发酵培养基(％)：葡萄糖2．酵母膏2,CaCO3,1．5,丙酸产量为9．35g／L,对糖的产率达51．94％,丙酸对乙酸的比例近5：l。     

产酸丙酸杆菌生长特性及5L罐发酵动力学研究

论文在摇瓶水平对产酸丙酸杆菌基本生长特性（温度、pH、摇床转速、接种量、种龄等）、碳源、氮源利用情况、产物抑制及5 L罐发酵动力学进行了研究。结果表明,该菌在32℃,初始pH 6．5,摇床转速150 r/min,接种24 h的种子液,接种量为5％条件下,产酸丙酸杆菌生长及产酸水平达最高值;该菌可利用碳源十分广泛,但对氮源要求比较高,只可利用有机氮源;在不同初始葡萄糖浓度下,产酸丙酸杆菌生长及产酸水平差异不大,无明显底物抑制现象;在2g/L的初始丙酸盐浓度下,该菌生长受到明显抑制;在5L发酵罐中,初始葡萄糖浓度为58．8 g/L,发酵72 h,葡萄糖消耗完全,丙酸终浓度达22．4 g/L,丙酸得率和产率分别达0．381 g/g和0．295 g/（L·h）,丙酸占总酸比例达72．10％。     

产酸丙酸杆菌FS1171产丙酸发酵动力学研究

对产酸丙酸杆菌（Propionibacterium acidogenes）FS1171产丙酸的分批发酵动力学进行研究,基于经典发酵动力学模型（Logistic、Luedeking-Piret、Dose-Resp方程）及Origin软件优选模型（Boltzmann方程）两种方法分别构建丙酸发酵过程中菌体生长、丙酸合成及底物甘油消耗随时间变化的动力学模型,软件分析表明,经典发酵动力学构建的模型拟合度整体不如Boltzmann方程构建的动力学模型,但前者所构建的3个动力学模型之间有较好的关联性,两种方法构建的模型拟合值和实验值能较好的吻合,说明所构建的产酸丙酸杆菌的发酵动力学能较好地反应丙酸杆菌的发酵过程,为优化发酵过程和工业上放大生产丙酸提供参考。     

产酸丙酸杆菌耐酸菌株的选育及其应用

为了解除微生物发酵生产丙酸过程中代谢产物(丙酸)对菌体生长的抑制作用,以实验室保藏的产酸丙酸杆菌(耐30g/L丙酸)为出发菌株P-0,通过丙酸压力筛选获得了一株耐10g/L丙酸的产酸性能良好的菌株P-10,降低了发酵过程中丙酸对菌体生长的抑制作用。菌株P-10做摇瓶发酵,发酵周期168h,丙酸浓度为49.66g/L,产酸速率为0.30g/(L·h),较出发菌株P-0提高了53.04%;7L发酵罐实验表明,菌株P-10发酵周期168h,丙酸浓度为55.63g/L,产酸速率0.33g/(L·h)。同时对菌株P-10做二次接种实验,结果表明,84h为二次接种最适时间段,且84h进行二次接种时,丙酸浓度提高了17.77%,二次接种实验不但有利于有机酸的积累,而且可以提高菌株的产酸能力和耐酸能力;经过选育的菌株P-10具有优良的产酸稳定性,有利于菌种的工业化生产和应用,同时对后续的发酵分离耦合具有重要意义。     

产酸丙酸杆菌耐酸菌株的选育及其应用

为了解除微生物发酵生产丙酸过程中代谢产物(丙酸)对菌体生长的抑制作用,以实验室保藏的产酸丙酸杆菌(耐30g/L丙酸)为出发菌株P-0,通过丙酸压力筛选获得了一株耐10g/L丙酸的产酸性能良好的菌株P-10,降低了发酵过程中丙酸对菌体生长的抑制作用。菌株P-10做摇瓶发酵,发酵周期168h,丙酸浓度为49.66g/L,产酸速率为0.30g/(L·h),较出发菌株P-0提高了53.04%;7L发酵罐实验表明,菌株P-10发酵周期168h,丙酸浓度为55.63g/L,产酸速率0.33g/(L·h)。同时对菌株P-10做二次接种实验,结果表明,84h为二次接种最适时间段,且84h进行二次接种时,丙酸浓度提高了17.77%,二次接种实验不但有利于有机酸的积累,而且可以提高菌株的产酸能力和耐酸能力;经过选育的菌株P-10具有优良的产酸稳定性,有利于菌种的工业化生产和应用,同时对后续的发酵分离耦合具有重要意义。     

海藻酸盐固定化北京丙酸杆菌丙酸发酵的研究

本文报道利用海藻酸钠固定化北京丙酸杆菌,及其丙酸发酵的最适条件。最适海藻酸钠和菌体的起始浓度分别为2％和I00％(w／v)。菌体和海藻酸盐混合滴入CaCl₂：溶液中得到直径为3—4 mm球形颗粒。将固定化细胞放入25ml厌氧管中5 g颗粒/15ml培养基。其成分为(％)：葡萄糖1,酵母膏0．5,CaCI₂0.1。30℃静置培养产生大量的挥发酸,丙酸对乙酸的比例接近10：1。固定化细胞重复利用发酵30次,保持稳定活性65天。     

丙酸杆菌属中的一个新种

从沼气发酵液中,分离出几株丙酸菌。该菌为革兰氏阳性、不形成芽孢的兼性厌氧菌。厌氧培养在BPYL培养基上细胞为球形;在BPY培养基上细胞则为杆状。能利用20多种糖和醇产酸,产生丙酸和乙酸。水解七叶苷,还原硝酸盐,过氧化氢酶阳性,不液化明胶,不产生吲哚。不利用D-阿拉伯糖和木糖产酸。该菌株属于丙酸杆菌属中的一个新种,定名为北京丙酸杆菌 Propionibacterium beijingense sp nov。     

低成本绿色循环工艺发酵生产丙酸联产维生素B12

对提取维生素B12后的费氏丙酸杆菌废菌体进行水解处理,考察以菌体水解液作为N源用于丙酸发酵的可行性.利用正交设计得到了提取维生素B12后的废菌体水解优化条件.基于此,构建利用植物纤维床反应器固定化生产丙酸联产维生素B12的低成本绿色循环工艺.结果表明:在4.5L的发酵体系中,单批次总糖质量浓度为200 g/L,发酵进行了5批次共1192h,丙酸生成总量为2 328.75 g,单批次丙酸质量浓度103.50 g/L,丙酸生产效率达0.43 g/(L·h),干菌质量浓度达到19.52 g/L.将菌体注入微好氧发酵罐中发酵获得112.8 mg/L维生素B12.     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

假蜜环菌液体深层发酵条件的研究

对该真菌菌丝体的液体深层培养条件进行了探讨为进一步工业化发酵提供参考数据。方法：在基本培养基的基础上分别改变碳源、氮源、无机元素和C／N比对该菌的液体深层发酵情况,包括测量各培养条件下耗糖情况、绘制生长曲线,观察菌体的生长形态等等。结果：假蜜环菌的菌丝产量在第6d可达到最大值,其后会逐渐降低,并伴有溶菌的现象发生。在培养初期加入微量钴元素有利于刺激糖代谢提高菌体对糖的利用率,其作用主要是缩短延滞期。进入指数生长期后连续补加碳源有利于菌体迅速生长。优化后培养基组成为：葡萄糖l％和蔗糖1％为碳源,以酵母浸膏l％为氮源,KH2PO4 0．1％,MgSO4 0．05％Z,元素钴适量。液体深层发酵培养6d后菌丝生长状态已达到最佳,在此条件下搅拌发酵培养可收获20mg/ml(干重)的菌丝体。     

Effect of fermentation inhibitors in the presence and absence of activated charcoal on the growth of Saccharomyces cerevisiae

The acidic hydrolysis of biomass generates numerous inhibitors of fermentation, which adversely affect cell growth and metabolism. The goal of the present study was to determine the effects of fermentation inhibitors on growth and glucose consumption by Saccharomyces cerevisiae. We also conducted in situ adsorption during cell cultivation in synthetic broth containing fermentation inhibitors. In order to evaluate the effect of in situ adsorption on cell growth, five inhibitors, namely 5-hydroxymethylfurfural, levulinic acid, furfural, formic acid, and acetic acid, were introduced into synthetic broth. The existence of fermentation inhibitors during cell culture adversely affects cell growth and sugar consumption. Furfural, formic acid, and acetic acid were the most potent inhibitors in our culture system. The in situ adsorption of inhibitors by the addition of activated charcoal to the synthetic broth increased cell growth and sugar consumption. Our results indicate that detoxification of fermentation media by in situ adsorption may be useful for enhancing biofuel production.     

Arginine catabolism by sourdough lactic acid bacteria: purification and characterization of the arginine deiminase pathway enzymes from Lactobacillus sanfranciscensis CB1

The cytoplasmic extracts of 70 strains of the most frequently isolated sourdough lactic acid bacteria were screened initially for arginine deiminase (ADI), ornithine transcarbamoylase (OTC), and carbamate kinase (CK) activities, which comprise the ADI (or arginine dihydrolase) pathway. Only obligately heterofermentative strains such as Lactobacillus sanfranciscensis CB1; Lactobacillus brevis AM1, AM8, and 10A; Lactobacillus hilgardii 51B; and Lactobacillus fructivorans DD3 and DA106 showed all three enzyme activities. Lactobacillus plantarum B14 did not show CK activity. L. sanfranciscensis CB1 showed the highest activities, and the three enzymes were purified from this microorganism to homogeneity by several chromatographic steps. ADI, OTC, and CK had apparent molecular masses of ca. 46, 39, and 37 kDa, respectively, and the pIs were in the range of 5.07 to 5.2. The OTCs, CKs, and especially ADIs were well adapted to pH (acidic, pH 3.5 to 4.5) and temperature (30 to 37 degrees C) conditions which are usually found during sourdough fermentation. Internal peptide sequences of the three enzymes had the highest level of homology with ADI, OTC, and CK of Lactobacillus sakei. L. sanfranciscensis CB1 expressed the ADI pathway either on MAM broth containing 17 mM arginine or during sourdough fermentation with 1 to 43 mM added arginine. Two-dimensional electrophoresis showed that ADI, OTC, and CK were induced by factors of ca. 10, 4, and 2 in the whole-cell extract of cells grown in MAM broth containing 17 mM arginine compared to cells cultivated without arginine. Arginine catabolism in L. sanfranciscensis CB1 depended on the presence of a carbon source and arginine; glucose at up to ca. 54 mM did not exert an inhibitory effect, and the pH was not relevant for induction. The pH of sourdoughs fermented by L. sanfranciscensis CB1 was dependent on the amount of arginine added to the dough. A low supply of arginine (6 mM) during sourdough fermentation by L. sanfranciscensis CB1 enhanced cell growth, cell survival during storage at 7 degrees C, and tolerance to acid environmental stress and favored the production of ornithine, which is an important precursor of crust aroma compounds.     

产琥珀酸重组大肠杆菌的发酵性能研究

研究了重组大肠杆菌JM001(△ppc)/pTrc99a-pck发酵产琥珀酸的性能,结果表明厌氧条件下其耗糖能力和产酸能力分别为对照菌株JM001的4.2倍和15.3倍。进一步优化发酵条件表明：采用接入菌泥的发酵方式比按照10%接种量转接厌氧发酵的效果要好,琥珀酸的对葡萄糖的质量收率提高了约10%,且副产物乙酸的量进一步降低。初始葡萄糖浓度高于60g/L时会对菌株的生长和产酸产生抑制,且浓度越高,抑制作用越明显。7L发酵罐放大实验中,整个厌氧发酵阶段葡萄糖的消耗速率为0.42g/(L.h),琥珀酸对葡萄糖的质量收率为67.75%,琥珀酸的生产强度为0.28g/(L.h)。     

过量表达NADH氧化酶加速光滑球拟酵母合成丙酮酸

[目的]进一步提高光滑球拟酵母(Torulopsis glabrata)发酵生产丙酮酸的生产强度.[方法]将来源于乳酸乳球菌(Lactococcus lactis)中编码形成水的NADH氧化酶noxE基因过量表达于丙酮酸工业生产菌株T. glabrata CCTCC M202019中,获得了一株NADH氧化酶活性为34.8 U/mg蛋白的重组菌T. glabrata-PDnoxE.[结果]与出发菌株T. glabrata CCTCC M202019相比,细胞浓度、葡萄糖消耗速率和丙酮酸生产强度分别提高了168%、44.9%和12%,发酵进行到36 h葡萄糖消耗完毕.补加50 g/L葡萄糖继续发酵20 h,则使丙酮酸浓度提高到67.2 g/L.葡萄糖消耗速度和丙酮酸生产强度增加的原因在于形成水的NADH氧化酶过量表达,导致NADH和ATP含量分别降低了18.1%和15.8%.而NAD<' 增加了11.1%.[结论]增加细胞内NAD<' 含量能有效地提高酵母细胞葡萄糖的代谢速度及目标代谢产物的生产强度.     

高山红景天细胞悬浮培养中红景天甙生物合成代谢的调控 Ⅰ:前体的影响

探索了高山红景天(Rhodiola sachalinensis A.Bor)细胞培养中红景天甙生物合成的途径,认为甙元酪醇是经由莽草酸途径生成的。在此基础上研究了酪醇、L-酪氨酸与L-苯丙氨酸三种前体加入对红景天甙生物合成的调控作用。结果表明,酪醇、酪氨酸等前体易被多酚氧化酶氧化成褐色,用与前体浓度为1:1的V。来防止褐化效果显著;浓度为0.5mmol/L的酪醇,酪氨酸及苯丙氨酸在细胞培养15d时添加,使红景天甙含量由0.336％分别提高到1.43％、1.11％、0.85％。     

High-cell-density cultivation of Schizochytrium sp. in an ammonium/pH-auxostat fed-batch system

Thraustochytrids, in particular Schizochytrium spp., are used for the production of the valuable polyunsaturated fatty acid, docosahexaenoic acid (DHA; 22:6 n-3). Growth of Schizochytrium sp. G13/2S in a defined medium was initially made in shake-flask cultures to determine the optimum concentrations of glucose (100-200 g l(-1)) and ammonia ( approximately 300 mg l(-1)) that could be used by this microorganism. In subsequent fermenter cultures, a pH-auxostat method was used to maintain NH(3) from 200-300 mg l(-1). During the first 49 h of fermentation, 150 g glucose l(-1) produced 63 g cell dry wt l(-1). Although growth was not limited by the supply of nitrogen, total fatty acids were at 25% cell dry wt which is more than half the final lipid content of commercially-grown Schizochytrium biomass which uses N-limited medium in the final stages for maximum lipid accumulation. This strategy is therefore useful for the cultivation of Schizochytrium to a high cell density up to the point when lipid accumulation can be triggered by N exhaustion.     

被孢霉生物合成花生四烯酸的初步研究

花生四烯酸不仅是细胞膜的重要成分,在维持细胞膜的结构与功能上发挥重要作用,而且是人体前列腺素合成的前体物质,对人体生理功能具有重要的调节作用。近年来研究发现,花生四烯酸在保护皮肤、降低胆固醇、抑制血小板聚集、提高免疫能力、促进胎儿发育等方面具有独特的...     

Measurement and analysis of intracellular ATP levels in metabolically engineered Zymomonas mobilis fermenting glucose and xylose mixtures

Intracellular adenosine-5'-triphosphate (ATP) levels were measured in a metabolically engineered Zymomonas mobilis over the course of batch fermentations of glucose and xylose mixtures. Fermentations were conducted over a range of pH (5-6) in the presence of varying initial amounts of acetic acid (0-8 g/L) using a 10% (w/v) total sugar concentration (glucose only, xylose only, or 5% glucose/5% xylose mixture). Over the design space investigated, ethanol process yields varied between 56.6% and 92.3% +/- 1.3% of theoretical, depending upon the test conditions. The large variation in process yields reflects the strong effect pH plays in modulating the inhibitory effect of acetic acid on fermentation performance. A corresponding effect was observed on maximum cellular specific growth rates, with the rates varying between a low of 0.15 h(-1) observed at pH 5 in the presence of 8 g/L acetic acid to a high of 0.32 +/- 0.02 h(-1) obtained at pH 5 or 6 when no acetic acid was initially present. While substantial differences were observed in intracellular specific ATP concentration profiles depending upon fermentation conditions, maximum intracellular ATP accumulation levels varied within a relatively narrow range (1.5-3.8 mg ATP/g dry cell mass). Xylose fermentations produced and accumulated ATP at much slower rates than mixed sugar fermentations (5% glucose, 5% xylose), and the ATP production and accumulation rates in the mixed sugar fermentations were slightly slower than in glucose fermentations. Results demonstrate that higher levels of acetic acid delay the onset and influence the extent of intracellular ATP accumulation. ATP production and accumulation rates were most sensitive to acetic acid at lower values of pH.     

In-situ recovery of butanol during fermentation

End product inhibition can be reduced by the in situ removal of inhibitory fermentation products as they form. Extractive fermentation, in which an immiscible organic solvent is added to the fermentor in order to extract inhibitory products, was applied to the acetone-butanol fermentation. Six solvents or solvent mixtures were tested in batch extractive fermentations: kerosene, 30 wt% tetradecanol in kerosene, 50 wt% dodecanol in kerosene, oleyl alcohol, 50 wt% oleyl alcohol in a decane fraction and 50 wt% oleyl alcohol in benzyl benzoate. The best results were obtained with oleyl alcohol or a mixture of oleyl alcohol and benzyl benzoate. In normal batch fermentation of Clostridium acetobutylicum, glucose consumption is limited to about 80 kg/m³ due to the accumulation of butanol in the broth. In extractive fermentation using oleyl alcohol or a mixture of oleyl alcohol and benzyl benzoate, over 100 kg/m³ of glucose can be fermented. Removal of butanol from the broth as it formed also increased the rate of butanol production. Maximum volumetric butanol productivity was increased by as much as 60% in extractive fermentation compared to batch fermentation. Butanol productivities obtained in extractive fermentation compare favorably with other in situ product removal fermentations.     

高山被孢霉三阶段培养法生产花生四烯酸油脂

为提高高山被孢霉（Mortierella alpina）生物合成花生四烯酸油脂的生产效率,基于花生四烯酸油脂的积累机制,建立了一种三阶段培养法：第一阶段在全培养基中培养促进菌体生物量的快速积累,确定了60 g/L糖初始质量浓度时,最有利于生物量的快速积累;第二阶段在C源丰富而其他营养缺乏的条件下培养,促进油脂快速积累,对糖最佳初始浓度、接种时间、pH和培养时间进行了优化;第三阶段培养诱导油脂中花生四烯酸的高效积累,并确定此阶段培养时间为36 h时为最佳时间。实验结果表明：三阶段培养工艺条件下,菌体生物量、油脂量、花生四烯酸量分别为41.6、26.6和11.4 g/L,本研究相比传统分批发酵工艺在产率和花生四烯酸最终产量方面都有了显著提高。